纯CuO/MgO体系和掺杂K+体系对2-丙醇转化的催化性能

S. A. El-Molla, G. El-Shobaky, N. H. Amin, M. N. Hammed, S. Sultan
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引用次数: 8

摘要

采用浸渍法制备了不同组分的CuO/MgO体系,并在400 ~ 900℃下进行了煅烧。采用XRD、N2在-196℃的吸附、150 ~ 400℃的流动技术转化异丙醇,考察了CuO含量、煅烧温度和少量K + (1 ~ 3 mol %)掺杂对体系理化性能、表面性能和催化性能的影响。结果表明:在400℃煅烧条件下,由纳米MgO和CuO为主相,Cu2O为次相组成的CuO/MgO配方为0.2和0.3;不同吸附剂的bet -表面积随CuO含量、煅烧温度和K +掺杂的增加而减小。mgo载体材料对2-丙醇转化的催化活性很小。该体系作为2-丙醇脱氢的选择性催化剂,选择性> 80%。在400 ~ 900℃范围内,随着CuO含量的增加,催化活性提高,随着焙烧温度的升高,催化活性降低。K + - p-
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Catalytic Properties of Pure and K+-Doped CuO/MgO System Towards 2-Propanol Conversion
CuO/MgO system having different compositions was pre- pared by impregnation method followed by calcination at 400-900 °C. The effect of CuO content, calcination temperature and doping with small amounts of K + species (1-3 mol %) on physicochemical, surface and catalytic properties of the system were investigated using XRD, adsorption of N2 at -196 °C, and conversion of isopropyl alcohol at 150-400 °C using a flow technique. The results revealed that the solids having the formulae 0.2 and 0.3 CuO/MgO calcined at 400 °C con- sisted of nanosized MgO and CuO as major phases together with Cu2O as minor phase. The BET-surface areas of different adsorbents are decreased by increasing CuO content, calcination temperature and K + - doping. MgO-support material showed very small catalytic activity in 2-propanol conversion. The investigated system behaved as selective catalyst for dehydrogenation of 2-propanol with selectivity > 80%. The catalytic activity increased by increasing CuO content and decreased by increasing the calcination temperature within 400-900 °C. K + - dop-
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